233 lines
6.9 KiB
C++
233 lines
6.9 KiB
C++
/**
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*
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* @file ThermoPhase.cpp
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*/
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/*
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* $Author$
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* $Date$
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* $Revision$
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*
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* Copyright 2002 California Institute of Technology
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*
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*/
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// turn off warnings under Windows
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#ifdef WIN32
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#pragma warning(disable:4786)
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#pragma warning(disable:4503)
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#endif
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#include "ThermoPhase.h"
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namespace Cantera {
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void ThermoPhase::getActivities(doublereal* a) {
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getActivityConcentrations(a);
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int nsp = nSpecies();
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int k;
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for (k = 0; k < nsp; k++) a[k] /= standardConcentration(k);
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}
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void ThermoPhase::setState_TPX(doublereal t, doublereal p,
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const doublereal* x) {
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setMoleFractions(x); setTemperature(t); setPressure(p);
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}
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void ThermoPhase::setState_TPX(doublereal t, doublereal p,
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compositionMap& x) {
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setMoleFractionsByName(x); setTemperature(t); setPressure(p);
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}
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void ThermoPhase::setState_TPX(doublereal t, doublereal p,
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const string& x) {
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compositionMap xx;
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int kk = nSpecies();
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for (int k = 0; k < kk; k++) xx[speciesName(k)] = -1.0;
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try {
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parseCompString(x, xx);
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}
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catch (CanteraError) {
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throw CanteraError("setState_TPX",
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"Unknown species in composition map: "+ x);
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}
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setMoleFractionsByName(xx); setTemperature(t); setPressure(p);
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}
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void ThermoPhase::setState_TPY(doublereal t, doublereal p,
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const doublereal* y) {
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setMassFractions(y); setTemperature(t); setPressure(p);
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}
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void ThermoPhase::setState_TPY(doublereal t, doublereal p,
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compositionMap& y) {
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setMassFractionsByName(y); setTemperature(t); setPressure(p);
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}
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void ThermoPhase::setState_TPY(doublereal t, doublereal p,
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const string& y) {
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compositionMap yy;
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int kk = nSpecies();
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for (int k = 0; k < kk; k++) yy[speciesName(k)] = -1.0;
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try {
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parseCompString(y, yy);
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}
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catch (CanteraError) {
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throw CanteraError("setState_TPY",
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"Unknown species in composition map: "+ y);
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}
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setMassFractionsByName(yy); setTemperature(t); setPressure(p);
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}
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void ThermoPhase::setState_TP(doublereal t, doublereal p) {
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setTemperature(t); setPressure(p);
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}
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void ThermoPhase::setState_PX(doublereal p, doublereal* x) {
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setMoleFractions(x); setPressure(p);
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}
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void ThermoPhase::setState_PY(doublereal p, doublereal* y) {
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setMassFractions(y); setPressure(p);
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}
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void ThermoPhase::setState_HP(doublereal h, doublereal p,
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doublereal tol) {
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doublereal dt;
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setPressure(p);
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for (int n = 0; n < 50; n++) {
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dt = (h - enthalpy_mass())/cp_mass();
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if (dt > 100.0) dt = 100.0;
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else if (dt < -100.0) dt = -100.0;
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setState_TP(temperature() + dt, p);
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if (fabs(dt) < tol) {
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return;
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}
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}
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throw CanteraError("setState_HP","no convergence. dt = " + fp2str(dt));
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}
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void ThermoPhase::setState_UV(doublereal u, doublereal v,
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doublereal tol) {
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doublereal dt;
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setDensity(1.0/v);
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for (int n = 0; n < 50; n++) {
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dt = (u - intEnergy_mass())/cv_mass();
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if (dt > 100.0) dt = 100.0;
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else if (dt < -100.0) dt = -100.0;
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setTemperature(temperature() + dt);
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if (fabs(dt) < tol) {
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return;
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}
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}
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throw CanteraError("setState_UV",
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"no convergence. dt = " + fp2str(dt)+"\n"
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+"u = "+fp2str(u)+" v = "+fp2str(v)+"\n");
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}
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void ThermoPhase::setState_SP(doublereal s, doublereal p,
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doublereal tol) {
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doublereal dt;
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setPressure(p);
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for (int n = 0; n < 50; n++) {
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dt = (s - entropy_mass())*temperature()/cp_mass();
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if (dt > 100.0) dt = 100.0;
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else if (dt < -100.0) dt = -100.0;
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setState_TP(temperature() + dt, p);
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if (fabs(dt) < tol) {
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return;
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}
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}
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throw CanteraError("setState_SP","no convergence. dt = " + fp2str(dt));
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}
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void ThermoPhase::setState_SV(doublereal s, doublereal v,
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doublereal tol) {
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doublereal dt;
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setDensity(1.0/v);
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for (int n = 0; n < 50; n++) {
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dt = (s - entropy_mass())*temperature()/cv_mass();
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if (dt > 100.0) dt = 100.0;
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else if (dt < -100.0) dt = -100.0;
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setTemperature(temperature() + dt);
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if (fabs(dt) < tol) {
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return;
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}
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}
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throw CanteraError("setState_SV","no convergence. dt = " + fp2str(dt));
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}
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doublereal ThermoPhase::err(string msg) const {
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throw CanteraError("ThermoPhase","Base class method "
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+msg+" called. Equation of state type: "+int2str(eosType()));
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return 0;
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}
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/**
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* Returns the units of the standard and general concentrations
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* Note they have the same units, as their divisor is
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* defined to be equal to the activity of the kth species
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* in the solution, which is unitless.
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*
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* This routine is used in print out applications where the
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* units are needed. Usually, MKS units are assumed throughout
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* the program and in the XML input files.
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*
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* On return uA contains the powers of the units (MKS assumed)
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* of the standard concentrations and generalized concentrations
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* for the kth species.
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*
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* uA[0] = kmol units - default = 1
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* uA[1] = m units - default = -nDim(), the number of spatial
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* dimensions in the Phase class.
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* uA[2] = kg units - default = 0;
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* uA[3] = Pa(pressure) units - default = 0;
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* uA[4] = Temperature units - default = 0;
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* uA[5] = time units - default = 0
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*/
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void ThermoPhase::getUnitsStandardConc(double *uA, int k, int sizeUA) {
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for (int i = 0; i < sizeUA; i++) {
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if (i == 0) uA[0] = 1.0;
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if (i == 1) uA[1] = -nDim();
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if (i == 2) uA[2] = 0.0;
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if (i == 3) uA[3] = 0.0;
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if (i == 4) uA[4] = 0.0;
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if (i == 5) uA[5] = 0.0;
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}
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}
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/**
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* Set the thermodynamic state.
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*/
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void ThermoPhase::setStateFromXML(const XML_Node& state) {
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string comp = getString(state,"moleFractions");
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if (comp != "")
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setMoleFractionsByName(comp);
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else {
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comp = getString(state,"massFractions");
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if (comp != "")
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setMassFractionsByName(comp);
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}
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if (state.hasChild("temperature")) {
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double t = getFloat(state, "temperature", "temperature");
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setTemperature(t);
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}
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if (state.hasChild("pressure")) {
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double p = getFloat(state, "pressure", "pressure");
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setPressure(p);
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}
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if (state.hasChild("density")) {
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double rho = getFloat(state, "density", "density");
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setDensity(rho);
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}
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}
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}
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